control of mercury emissions by injecting powdered activated carbon (pac)
DESCRIPTION
Control of Mercury Emissions by Injecting Powdered Activated Carbon (PAC). Presentation to Utility MACT Working Group May 13, 2002 EPA, RTP, NC. Michael D. Durham, Ph.D., MBA ADA Environmental Solutions 8100 SouthPark Way B-2 Littleton, CO 80120 303 734-1727. Outline. - PowerPoint PPT PresentationTRANSCRIPT
Control of Mercury Emissions
by Injecting Powdered Activated Carbon (PAC)
Michael D. Durham, Ph.D., MBAADA Environmental Solutions
8100 SouthPark Way B-2Littleton, CO 80120
303 734-1727
Presentation to Utility MACT Working Group
May 13, 2002EPA, RTP, NC
Outline
ADA-ES DOE/NETL Hg Control Program
Background on PAC Injection Technology
Results from PAC with an ESP
Results from PAC with a FF
Conclusions and Future Plans
ADA-ES Hg Control Program Full-scale field testing of sorbent-based mercury control on non-
scrubbed coal-fired boilers
Primary funding from DOE National Energy Technology Laboratory (NETL)
Cofunding provided by:– Southern Company – Wisconsin Electric– PG&E NEG– EPRI– Ontario Power Generation– TVA– First Energy– Kennecott Energy– Arch Coal
Project Overview
Perform first full-scale evaluations of mercury control on coal-fired boilers (up to 150 MW equivalent).
Evaluate effectiveness of sorbent-based Hg control (activated carbon).
Test several different power plant configurations.
Document all costs associated with Hg control.
DOE/NETL Test SitesTest Site Coal Particulate Test
Control DatesAlabama Power Bituminous HS ESP SpringGaston COHPAC FF 2001Wisconsin Electric PRB Cold Side ESP FallPleasant Prairie 2001PG&E NEG Bituminous Cold Side ESP SummerBrayton Point 2002PG&E NEG Bituminous Cold Side ESP FallSalem Harbor 2002
Coal-Fired Boiler with Sorbent Injection and Spray Cooling
Sorbent Injection
Spray Cooling
H2O
Air
Ash and Sorbent
ESP or FF
Hg CEM
Semi-Continuous Mercury Analyzer
Chilled Impingers
Flue GasCVAA
Mass Flow Controller
Gold Trap
Waste
Heater
Micro controller with Display
Dry Air
Sampling Time Required
Vapor-Phase Mercury
Concentration (ug/m3)
Minimum Sample Time (min)
Noise level (ug/m3)
5 1 0.1
2.5 2 0.05
1 5 0.02
0.5 10 0.01
Comparison of OH and S-CEM*, Long Term Tests (10 lbs/MMacf)
Run Number Run 1 Run 2 Run 3 AverageDate 11/12/2001 11/13/2001 11/13/2001
S-CEM* OH S-CEM* OH S-CEM* OH S-CEM* OHInlet (micrograms/dncm) 13.5 15 13.7 18.3 14.3 19.1 13.8 17.4Outlet (micrograms/dncm) 4.8 4.0 5.1 5.0 5.4 4.7 5.1 4.7Removal Efficiency (%) 64.4% 73.4% 62.8% 72.8% 64.0% 75.3% 63.7% 72.9%
* S-CEM measures only gas phase mercury, average calculated over same time as OH tests
Capture of Vapor Phase Hg by Solid Sorbents
Mass Transfer Limits (getting the Hg to the sorbent)
– Removal increases with particle concentration
– Produces percentage removal independent of concentration
– Particle control device (FF vs ESP) is a critical parameter
Sorbent Capacity to hold Hg depends upon:
– Sorbent characteristics
– Temperature
– Mercury concentration
– Concentrations of SO3 and other contaminants
Equilibrium Adsorption Capacities at 250°FUpstream and Downstream of SO3 Injection
0
1000
2000
3000
4000
5000
6000
7000
8000
9000
10000
FGD Carbon Norit Insul Carbon P4 Ash
Equi
libriu
m A
dsor
ptio
n C
apac
ity a
t 50m
g/N
m3 (µ
g H
g/g)
Upstream ofSO3
Downstream ofSO3
WEPCO Pleasant Prairie Testing completed fall of 2001 PRB coal ESP only Spray cooling SO3 conditioning system
Activated Carbon Storage and Feed System
ESP Configuration, PPPP
ESP 2-4
Spray Cooling
Carbon Injection
Powdered Activated Carbon Injection System
Baseline Hg Measurements (mg/dscm)
Location Particle Bound
Oxidized, Hg2+
Elemental, Hg0
Total, Hg
Inlet ’99 0.16 2.29 6.21 8.65
Inlet ‘01 1.84 2.34 11.39 15.55
Mercury Trends Week 1
0
5
10
9/24 9/24 9/25 9/25 9/26 9/26 9/27 9/27 9/28 9/28 9/29
Hg
(µg/
Nm3 )
0
10
20
30
40
lb/M
mac
f Sor
bent
Inlet Outlet Feeder
200
300
400
500
600
700
9/24 9/24 9/25 9/25 9/26 9/26 9/27 9/27 9/28 9/28 9/29
Load
(MW
)
250260270280290300310320
9/24 9/25 9/26 9/27 9/28 9/29
Tem
pera
ture
(F) Inlet Hg Probe Temp Outlet Hg Probe Temp
Response Time for PAC Injection on an ESP
0
4
8
12
16
6:00 10:00 14:00 18:00 22:00
Tota
l Hg
(µg/
dNm
3 )
0
10
20
30
40
lbs/
Mm
acf S
orbe
ntESP Inlet
ESP Outlet
Carbon Injection Performance on a PRB Coal with an ESP
0
10
20
30
40
50
60
70
80
0 10 20 30 40 50Injection Concentration (lb/MMacf)
% H
g R
emov
al
FGDFGD humidFGD(g)FGLFGD, no SO3FGD(g), no SO3InsulLong Term TestsOntario Hydro
Long Term Trend Data
0
5
10
15
20
10/29 11/5 11/12
Hg
(ug/
dNm3 )
0
5
10
15
20
Inj.
Con
c. (l
b/M
Mac
f)ESP Outlet Total ESP Inlet Total Inj. Conc.
020406080
100
10/29/01 11/5/01 11/12/01
Hg
Rem
. (%
)
300
500
700
10/29/01 11/5/01 11/12/01
Load
(MW
)
Speciated Mercury Measured by Ontario Hydro Method (10 lbs/MMacf)
PARTICULATE ELEMENTAL OXIDIZED TOTAL
Baseline ESP Inlet 1.97 12.22 2.51 16.71 ESP Outlet 0.01 9.80 6.01 15.82 Removal Efficiency 99.5% 19.8% -139.3 5.3%
(microgram/dncm)
PAC Injection ESP Inlet 0.98 14.73 1.73 17.44 ESP Outlet 0.00 4.27 0.44 4.71 Removal Efficiency 100.0% 71.0% 74.5% 73.0%
Alabama Power E.C. Gaston Alabama Power Company E.C.
Gaston Electric Generating Plant Unit 3, Wilsonville, AL
270 MW Firing a Variety of Low-Sulfur, Washed Eastern Bituminous Coals
Particulate Collection System– Hot-side ESP, SCA = 274 ft2/1000
acfm– COHPAC baghouse supplied by
Hamon Research-Cottrell
Wet Ash Disposal to Pond
Site Test Configuration with EPRI TOXECON at Alabama Power Plant Gaston
Sorbent Injection
COHPAC
Fly Ash (2%) + PAC
Coal
Fly Ash (98%)
ElectrostaticPrecipitator
S-CEM Duct Traverse
0
2
4
6
8
10
12
14
16
4/28/01 12:00 4/29/01 0:00 4/29/01 12:00 4/30/01 0:00
Hg (u
g/Nm
3)
Inlet Total
Inlet Elemental
Change Point
Example of S-CEM Data
0
5
10
15
20
3/12/2001 3/13/2001 3/14/2001 3/15/2001
Hg
(g/
Nm
3 )
012345
Inj.
Con
c. (l
b/M
Mac
f)
Total Inlet
Total Outlet
Injection Conc.
Response Time of PAC Injection with a Fabric Filter
0
10
20
4:00 8:00 12:00 16:00 20:00 0:00
Hg
(ug/
Nm
3 ) 3%
O2
0
1
2
3
Inj.
Conc
. (lb
/MM
acf)
Total Outlet Total Inlet Inj. Conc.
Mercury Removal vs. Injection Rate
0
10
20
30
40
50
60
70
80
90
100
0 1 2 3 4 5
Injection Concentration (lb/MMacf)
% H
g R
emov
al
Pressure Drop Increase from PAC Injection
0.0
0.5
1.0
1.5
2.0
2.5
3.0
3.5
4.0
4.5
0 0.5 1 1.5 2 2.5 3 3.5 4
Injection Concentration (lb/MMacf)
Avg
. pul
ses/
bag/
hr
Mercury Removal vs. Injection Rate
0
10
20
30
40
50
60
70
80
90
100
0 1 2 3 4 5
Injection Concentration (lb/MMacf)
% H
g R
emov
al
PAC Rate Limit Due to Pressure Drop
5-Day Continuous Injection
0
5
10
15
20
25
4/22 4/23 4/24 4/25 4/26 4/27
Hg
(µg/
Nm
3 )
Total Inlet
Total Outlet
Ontario Hydro
050
100150200250300
4/22 4/23 4/24 4/25 4/26 4/27
Boi
ler L
oad
(MW
)
024681012
Inj.
Con
c. (l
b/M
Mac
f)
Load
Sorbent Injection Concentration
Average Mercury Removal Long-Term Tests Gaston, Ontario Hydro
(microgram/dncm)PARTICULATE OXIDIZED ELEMENTAL TOTAL
Baseline COHPAC Inlet 0.09 9.54 5.97 15.60 COHPAC Outlet 0.01 11.19 3.34 14.54 Removal Efficiency 89.1% -17.3% 44.1% 6.8%
PAC Injection COHPAC Inlet 0.23 6.37 4.59 11.19 COHPAC Outlet 0.12 0.91 0.03 1.05 Removal Efficiency 45.6% 85.7% 99.3% 90.6%
Comparison of Sorbent Costs for a Fabric Filter and an ESP
020406080
100
0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6Sorbent Costs (US$/MWh)
% H
g R
emov
al
ESP
COHPAC FF
Conclusions (PAC General) PAC injection can effectively capture elemental and oxidized
mercury from both bituminous and subbituminous coals Additional field tests and long-term demonstrations are
necessary to continue to mature the technology Fabric filters provide better contact between the sorbent and
mercury than ESPs resulting in higher removal levels at lower sorbent costs
New COHPAC FF’s will have to be designed to handle higher loadings of PAC to insure high (>90%) mercury removal
Conventional FF’s should not require any modifications for PAC
Conclusions (Response to Concentration Variations)
Response times to changes in inlet concentrations:– Feedback data from outlet CEMs—tens of minutes– Impact of changes in injection rate: tens of minutes to hours
Long averaging times will be required to recover from upsets Injection at somewhat higher rates will make the technology
more capable to handle inlet fluctuations PAC injection lends itself to the use of feed rate parameters as
a definition of Maximum Achievable Control Technology
Future PlansShort-term testing at additional sites
–PG&E Brayton Point (Bituminous coal, large ESP) 6/ 2002–PG&E Salem Harbor (Bituminous coal, SNCR, large ESP) 9/2002–* TBD (PRB coal, small ESP) 3/2003–* Southern Company (Bituminous coal, small ESP) 8/ 2003
Long-term testing–*Alabama Power (Bituminous coal, COHPAC FF) 2002-2003–*CCPI Program (PRB Coal, COHPAC FF) 2004-2006–*CCPI Program (Bituminous Coal, COHPAC FF) 2004-2006
* Proposed
For More Information www.adaes.com www.adaes.com/mercury.htm
– Link to other mercury related web sites– Publications/reports
www.adaes.com/MercuryPublic.htm– Public information on DOE/NETL
Mercury Control Program www.netl.doe.gov/products/environment/index.html
DOE/NETL Website